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公开(公告)号:DE4302992A1
公开(公告)日:1994-08-04
申请号:DE4302992
申请日:1993-02-03
Applicant: BASF AG
Inventor: TENTEN ANDREAS DR , HAMMON ULRICH DR , WEIDLICH PETER DR , DOERFLINGER WALTER
IPC: B01J23/85 , B01J23/88 , B01J23/92 , B01J23/94 , B01J38/48 , B01J38/52 , B01J38/62 , B01J38/68 , C07C57/055
Abstract: Process for regenerating spent multimetal oxide oxidation catalysts from catalytic gas-phase oxidations of lower organic compounds, which catalysts, unspent, contain as base constituents the elements Mo, W, V and Cu in oxide form, by the action of oxidising agents and of solubilising aqueous ammonia containing added acetic acid and/or the ammonium salt thereof and subsequent drying and calcination in which, within the process, the content of the metallic constituents is quantitatively determined and supplemented to the respective original value.
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公开(公告)号:CZ386792A3
公开(公告)日:1993-12-15
申请号:CS386792
申请日:1992-12-23
Applicant: BASF AG
Inventor: DUEMBGEN GERD DR , FIEDLER ECKHARD DR , HAMMON ULRICH DR , THIESSEN FRITZ DR , VOGEL HERBERT DR
IPC: C07C51/44 , C07C51/487 , C07C51/50 , C07C57/04 , C07C57/055 , C07C57/07
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公开(公告)号:DE4201697A1
公开(公告)日:1993-07-29
申请号:DE4201697
申请日:1992-01-23
Applicant: BASF AG
Inventor: DUEMBGEN GERD DR , FIEDLER ECKHARD DR , HAMMON ULRICH DR , THIESSEN FRITZ DR , VOGEL HERBERT DR
IPC: C07C51/44 , C07C51/487 , C07C51/50 , C07C57/04 , C07C57/055 , C07C57/07
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公开(公告)号:DE4132684A1
公开(公告)日:1993-04-08
申请号:DE4132684
申请日:1991-10-01
Applicant: BASF AG
Inventor: HAMMON ULRICH DR , HERZOG KLAUS DR , NEUMANN HANS-PETER DR
IPC: C07C51/235 , B01J27/186 , B01J27/188 , B01J27/19 , B01J27/195 , B01J27/199 , C07C51/25 , C07C57/04 , C07C57/055
Abstract: A process for the catalytic gas-phase oxidation of methacrolein to methacrylic acid in a fixed-bed reactor with contacting tubes, at elevated temperature on catalytically active oxides with a conversion of methacrolein for a single pass of from 40 to 95 mol%, wherein the reaction temperature in the flow direction along the contacting tubes in a first reaction zone from entry of the starting reaction gases containing the reactants into the contacting tubes is from 280 to 340 DEG C. until a methacrolein conversion of from 20 to 40% is reached, and the reaction temperature is subsequently reduced by a total of from 5 DEG to 40 DEG C., abruptly or successively in steps or continuously along the contacting tubes until a methacrolein conversion of from 45 to 95% has been reached, with the proviso that the reaction temperature in this second reaction zone is not lower than 260 DEG C.
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公开(公告)号:MY147742A
公开(公告)日:2013-01-15
申请号:MYPI20083643
申请日:2004-04-14
Applicant: BASF AG
Inventor: DIEHL VOLKER DR , JAEGER ULRICH DR , HAMMON ULRICH DR , SCHROEDER JUERGEN DR , RISSEL STEFFEN
Abstract: A SEPARATING COLUMN CONTAINING A SEQUENCE OF MASS TRANSFER TRAYS THAT ARE SUPPORTED BY AT LEAST ONE COVERED DOUBLE-T SUPPORT (1) AND/OR COVERED U-SHAPED SUPPORT.
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公开(公告)号:MY121878A
公开(公告)日:2006-02-28
申请号:MYPI20000659
申请日:2000-02-23
Applicant: BASF AG
Inventor: UNVERRICHT SIGNE DR , ARNOLD HEIKO DR , TENTEN ANDREAS DR , HAMMON ULRICH DR , NEUMANN HANS-PETER DR , HARTH KLAUS DR
IPC: B01J23/88 , C07C51/25 , B01J23/00 , B01J23/31 , B01J23/887 , B01J35/00 , C07B61/00 , C07C27/14 , C07C45/35 , C07C47/22 , C07C51/215 , C07C57/04 , C07C57/05
Abstract: A PROCESS FOR THE CATALYTIC GAS-PHASE OXIDATION OF PROPENE TO ACRYLIC ACID, IN WHICH THE REACTION GAS STARTING MIXTURE IS OXIDIZED, WITH AN INCREASED PROPENE LOADING, IN A FIRST REACTION STAGE, OVER A FIRST FIXED-BED CATALYST AND THEN THE ACROLEIN-COATING PRODUCT GAS MIXTURE OF THE FIRST REACTION STAGE IS OXIDIZED, IN A SECOND REACTION STAGE, WITH AN INCREASED ACROLEIN LOADING, OVER A SECOND FIXED-BED CATALYST, THE CATALYST MOLDINGS IN BOTH REACTION STAGES HAVING AN ANNULAR GEMETRY.
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17.
公开(公告)号:MY116119A
公开(公告)日:2003-11-28
申请号:MYPI19972788
申请日:1997-06-20
Applicant: BASF AG
Inventor: HAMMON ULRICH DR , RAUH ULRICH , SCHLIEPHAKE VOLKER DR , PIES WOLFGANG DR
Abstract: IN A PROCESS FOR THE DISPOSAL OF LOW, MEDIUM, AND HIGH-BOILING SECONDARY COMPONENTS (1,2,3) FORMED DURING THE PREPARATION OF (METH) ACRYLIC ACID THE GASEOUS LOW BOILING SECONDARY COMPONENTS (2) ARE BURNED, WHILST LOW-BOILING AND MEDIUM-BOILING SECONDARY COMPONENTS (2) THAT ARE DISSOLVED IN WATER OPTIONALLY TOGETHER WITH HIGH-BOILING SECONDARY COMPONENTS (3) TREATED WITH SOLVENT ARE ADDED. (FIGURE 1)
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公开(公告)号:DE19717165A1
公开(公告)日:1998-10-29
申请号:DE19717165
申请日:1997-04-23
Applicant: BASF AG
Inventor: SCHLIEPHAKE VOLKER DR , HAMMON ULRICH DR , RAUH ULRICH , SCHRAUT ARMIN DR
Abstract: Reactor arrangement comprises at least two tubular reactors filled with solid particles, at least one reactor containing a temperature measuring device. The novelty is that the tubular reactors are arranged so that the ratio of the composition of the solid particles to the free cross-sectional surfaces of each reactor as well as the pressure loss, measured by passing an inert gas proportionally transversal to the free cross-sectional, are equal over each tubular reactor. Also claimed is a process for treating fluid compositions with the production and consumption of thermal energy using the above reactor arrangement.
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公开(公告)号:DE59600212D1
公开(公告)日:1998-07-02
申请号:DE59600212
申请日:1996-01-13
Applicant: BASF AG
Inventor: HERBST HOLGER DR , HAMMON ULRICH DR
Abstract: In the sepn. of (meth)acrylic acid (I) from mixts. contg. (I) as main prod. and lower aldehydes as by-prods. by rectification in a column with a distn. zone and a concn. zone, the mixt. is not supplied to the column directly. Instead, it is passed to a heated dwell vessel connected to the concn. zone, in which the mixt. is kept boiling, and the sump liquid from this vessel is fed to the column.
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公开(公告)号:DE59405671D1
公开(公告)日:1998-05-20
申请号:DE59405671
申请日:1994-01-25
Applicant: BASF AG
Inventor: TENTEN ANDREAS DR , HAMMON ULRICH DR , WEIDLICH PETER DR , DOERFLINGER WALTER
IPC: B01J23/85 , B01J23/88 , B01J23/92 , B01J23/94 , B01J38/48 , B01J38/52 , B01J38/62 , B01J38/68 , C07C57/055
Abstract: Process for regenerating spent multimetal oxide oxidation catalysts from catalytic gas-phase oxidations of lower organic compounds, which catalysts, unspent, contain as base constituents the elements Mo, W, V and Cu in oxide form, by the action of oxidising agents and of solubilising aqueous ammonia containing added acetic acid and/or the ammonium salt thereof and subsequent drying and calcination in which, within the process, the content of the metallic constituents is quantitatively determined and supplemented to the respective original value.
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